TW201350508A - Process for the manufacture of cyclic undecapeptides - Google Patents
Process for the manufacture of cyclic undecapeptides Download PDFInfo
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Abstract
Description
本發明係關於適用於環孢菌素衍生物之開環及隨後用於製備環狀多肽,更具體而言環狀十一胺基酸肽諸如阿拉泊韋(亦稱為DEB025、Debio025或Debio)之新穎方法、新穎製程步驟及新穎中間產物。 The present invention relates to ring opening suitable for use in cyclosporin derivatives and subsequent use in the preparation of cyclic polypeptides, more particularly cyclic undecyl acid peptides such as alisporivir (also known as DEB025, Debio025 or Debio). Novel methods, novel process steps, and novel intermediates.
本發明係關於製備環狀多肽諸如環狀十一胺基酸肽(諸如阿拉泊韋)之方法。 The present invention relates to a process for the preparation of a cyclic polypeptide such as a cyclic undecyl acid peptide such as alisporivir.
如WO 2006/038088中所述,阿拉泊韋為一種用於治療C型肝炎病毒(HCV)感染或經HCV誘發之疾病的親環素(Cyp)抑制劑。而且,WO2009/042892敘述阿拉泊韋用於治療多發性硬化症之方法;WO2009/098577敘述阿拉泊韋用於治療肌肉失養症之方法;WO2008/084368敘述阿拉泊韋用於治療Ullrich型先天性肌肉失養症之方法。 As described in WO 2006/038088, alisporivir is a cyclophilin (Cyp) inhibitor for the treatment of hepatitis C virus (HCV) infection or HCV-induced diseases. Furthermore, WO 2009/042892 describes a method for the treatment of multiple sclerosis by alisporivir; WO 2009/098577 describes a method for the treatment of muscle dystrophy by alisporivir; WO 2008/084368 describes rapavivir for the treatment of Ullrich type congenitality The method of muscle dystrophy.
WO 00/01715敘述阿拉泊韋及其合成法。阿拉泊韋已經分配CAS註冊號254435-95-5。 WO 00/01715 describes alisporivir and its synthesis. Alippo has assigned CAS registration number 254435-95-5.
J.F.Guichoux在「De nouveaux analogues de Cycloposrine A comme agent anti-HIV-1」PhD thesis,Faculte des Sciences de L’Universite de Lausanne,2002中,於WO2006/038088中及於 WO2008/084368中敘述實驗室規模之阿拉泊韋之製備方法。 J.F. Guichoux in "De nouveaux analogues de Cycloposrine A comme agent anti-HIV-1" PhD thesis, Faculte des Sciences de L'Universite de Lausanne, 2002, in WO2006/038088 A method for the preparation of laboratory-scale alisporivir is described in WO 2008/084368.
以下表示之環狀十一胺基酸肽為式(Ia)之環狀多肽,其中n=2。 The cyclic undecyl acid peptide shown below is a cyclic polypeptide of the formula (Ia) wherein n = 2.
阿拉泊韋(式I)為一種式(Ib)之環狀十一胺基酸肽,其中n=2,aa1為D-MeAla及aa2為EtVal。 Alaptop (Formula I) is a cyclic undecylamino acid peptide of formula (Ib) wherein n = 2, aa1 is D-MeAla and aa2 is EtVal.
通式:環 -(AXX1-AXX2-AXX3-AXX4-AXX5-AXX6-AXX-7-AXX8-AXX9-AXX10-AXX11)應涵蓋來自如在重要Sar片段處進行之片段化之案例WO2010/052559 A1的實例 General formula: Ring-(AXX1-AXX2-AXX3-AXX4-AXX5-AXX6-AXX-7-AXX8-AXX9-AXX10-AXX11) should cover cases from the fragmentation of the important Sar fragment, WO2010/052559 A1 Instance
AXX1=MeBmt、Bmt、MeLeu、脫氧-MeBmt、甲基胺基辛酸 AXX1=MeBmt, Bmt, MeLeu, Deoxy-MeBmt, Methylaminooctanoic acid
AXX2=Abu、Ala、Thr、Val、Nva AXX2=Abu, Ala, Thr, Val, Nva
AXX3=Sar AXX3=Sar
AXX4=MeLeu、Val AXX4=MeLeu, Val
AXX5=Val、Nva AXX5=Val, Nva
AXX6=MeLeu、Leu AXX6=MeLeu, Leu
AXX7=Ala、Abu AXX7=Ala, Abu
AXX8=D-Ala AXX8=D-Ala
AXX9=MeLeu、Leu AXX9=MeLeu, Leu
AXX10=MeLeu、Leu AXX10=MeLeu, Leu
AXX11=MeVal、Val、D-MeVal, 及在WO 2010/052559 A1中涵蓋之所有其他組合。 AXX11=MeVal, Val, D-MeVal, And all other combinations covered in WO 2010/052559 A1.
在最近幾年,環孢菌素A(CyA)已經用作各種適用於治療炎性或病毒疾病之合成環狀十一胺基酸肽的原料。環狀十一胺基酸肽可藉由菌株選育獲得,然而,獲得最不天然衍生物需要化學轉換,其依靠例如式(Ia)或式(Ib)之環狀多肽之開環及隨後胺基酸替代。 In recent years, cyclosporin A (CyA) has been used as a raw material for various synthetic cyclic undecapeptides suitable for the treatment of inflammatory or viral diseases. Cyclic undecaned acid peptides can be obtained by strain selection, however, obtaining the most natural derivatives requires chemical conversion, which relies on ring opening of a cyclic polypeptide such as formula (Ia) or (Ib) and subsequent amines Base acid substitution.
傳統上,例如式(Ia)之環狀多肽在高度選擇性方法中開環及經由埃德曼降解反應(Edman degradation)移除胺基酸殘基以獲得作為重要中間產物之開環的環狀多肽(Wenger,R.M.In Peptides 1996;Ramage,R.、Epton,R.編輯;The European Peptides Society,1996,第173頁;Wenger,R.M.等人,Tetrahedron Letters 2000,41,7193.)。許多科學家及公司已經利用該可靠及選擇性策略,其中純環孢菌素A及藉由柱狀層析法之純化已經用於獲得環狀十一胺基酸肽。 Conventionally, for example, a cyclic polypeptide of the formula (Ia) is ring-opened in a highly selective process and the amino acid residue is removed via an Edman degradation to obtain an open-loop ring as an important intermediate product. Polypeptide (Wenger, RM In Peptides 1996; Ramage, R., Epton, R. Ed.; The European Peptides Society, 1996, p. 173; Wenger, RM et al, Tetrahedron Letters 2000, 41, 7193.). Many scientists and companies have utilized this reliable and selective strategy in which pure cyclosporin A and purification by column chromatography have been used to obtain cyclic undecaned acid peptides.
而且,產物(諸如開環的環孢菌素A)之純化涉及若干藉由矽膠液體層析法純化之步驟。除了獲得適中的總產率,該純化方案之主要缺點在於層析法步驟之極高成本。文獻中所述之衍生自環孢菌素A或其結構類似物之該等產物的大規模純化方法一般涉及層析純化或至少一種藉由吸附層析法之前期純化。該前期純化之後可進行例如萃取、逆流萃取及/或超臨界流體萃取。 Moreover, purification of the product, such as ring-opened cyclosporin A, involves several steps of purification by gelatin liquid chromatography. In addition to obtaining moderate overall yields, the main disadvantage of this purification scheme is the extremely high cost of the chromatography steps. Large-scale purification methods of such products derived from cyclosporin A or its structural analogs described in the literature generally involve chromatographic purification or at least one prior purification by adsorption chromatography. This pre-purification can be followed by, for example, extraction, countercurrent extraction, and/or supercritical fluid extraction.
然而,由於需要高品質的昂貴前驅物,該等技術中沒有任一者 在所需品質要求、在可接受的總產率及在工業規模製造可接受的成本下獲得關鍵性開環的中間產物方面會完全令人滿意。 However, due to the need for high quality, expensive precursors, none of these technologies It would be entirely satisfactory to obtain critical ring-opening intermediates at the desired quality requirements, at acceptable total yields, and at acceptable cost to industrial scale manufacturing.
吾人發現二甲氧基碳正離子(在諾華(Novartis)專利申請案EP 0 908 461 A1中所述,用於頭孢菌素(Cephalosporine)衍生物之甲基化)在大環多肽之開環中進行與氧鎓離子(三甲基或三乙基氧鎓米爾文(Meerwein)鹽)相同的化學過程。新穎條件可有利地在原位製備,因此可避免處理有毒及吸濕物質、可在多種溶劑(諸如甲苯、二甲苯、苯胺)中進行、無需使用非所需的氯化溶劑(諸如二氯甲烷或二氯乙烷),及避免使用來源於遺傳毒性表氯醇之氧鎓米爾文鹽。專用的四氟硼酸碳或藉由三氟化硼與原酸酯衍生物(較佳係原甲酸三甲酯)之反應原位產生的反應性物質會產生所需的開環多肽(諸如以下化合物3)。 We have found that dimethoxy carbon cations (described in the Novartis patent application EP 0 908 461 A1 for methylation of Cephalosporine derivatives) are in the ring opening of macrocyclic polypeptides. The same chemical process as the oxonium ion (trimethyl or triethyloxan Meerwein salt) was carried out. The novel conditions can advantageously be prepared in situ, thus avoiding the handling of toxic and hygroscopic materials, can be carried out in a variety of solvents such as toluene, xylene, aniline, without the use of undesirable chlorinated solvents such as methylene chloride. Or dichloroethane), and avoid the use of oxy-mirrion salts derived from genotoxic epichlorohydrin. Dedicated tetrafluoroborate carbon or a reactive species produced in situ by reaction of boron trifluoride with an orthoester derivative, preferably trimethyl orthoformate, produces the desired ring-opening polypeptide (such as the following compounds) 3).
吾人發現一種保持高度選擇性埃德曼降解反應策略之優勢同時充分利用新識別之晶型中間產物之優勢的改良方法。 We have found an improved method that maintains the advantages of a highly selective Edman degradation reaction strategy while taking advantage of the newly identified crystalline intermediates.
以下揭示內容說明衍生自如下各者之開環之新單離及晶型中間產物: 環孢菌素A、 環孢菌素B、 環孢菌素D、 或環孢菌素G,及一種用以產生及經由諸如結晶之方法純化其之方法。該方法容許快速、實際及更高效地獲得開環的環孢菌素A、環孢菌素B、環孢菌素D或環孢菌素G及可用於製備環狀十一胺基酸肽(諸如阿拉泊韋)。而且,根據本揭示案之方法亦可應用至可經由相同順序開環之其他環孢菌素。據發現,開環的環孢菌素鹽(諸如鹽酸(HCl)、氟硼酸(HBF4)或六氟磷酸(HPF6))可在若干階段形成。 The following disclosure illustrates the novel open and crystalline intermediates derived from the ring opening of: cyclosporin A Cyclosporin B Cyclosporin D Cyclosporin G And a method for producing and purifying it via a method such as crystallization. The method allows for rapid, practical and more efficient obtaining of ring-opened cyclosporin A, cyclosporin B, cyclosporin D or cyclosporin G and for the preparation of cyclic undecyl acid peptides ( Such as Alippo). Moreover, the method according to the present disclosure can also be applied to other cyclosporins which can be opened by the same sequence. It has been found that a ring-opened cyclosporin salt such as hydrochloric acid (HCl), fluoroboric acid (HBF 4 ) or hexafluorophosphoric acid (HPF 6 ) can be formed in several stages.
本發明提供新穎的晶型中間產物,諸如環孢菌素酯,諸如乙酸酯、特戊酸酯,及開環的環孢菌素A、環孢菌素B、環孢菌素D或環孢菌素G鹽(諸如HCl鹽、HBF4鹽或HPF6鹽),及產生其之方法。 The present invention provides novel crystalline intermediates such as cyclosporin esters such as acetate, pivalate, and ring-opened cyclosporin A, cyclosporin B, cyclosporin D or a ring A sporein G salt (such as an HCl salt, a HBF 4 salt or an HPF 6 salt), and a method of producing the same.
本發明提供一種製備式3之化合物或其鹽的方法,
本發明提供一種製備式4之化合物或其鹽的方法,
本發明提供一種製備式4之化合物或其鹽的方法,
本發明提供一種式3之化合物或其鹽,
本發明提供一種式4之化合物或其鹽,
圖1為化合物3之質子NMR光譜。 Figure 1 is a proton NMR spectrum of Compound 3.
圖2為化合物4之質子NMR光譜。 2 is a proton NMR spectrum of Compound 4.
以下反應圖顯示用於製備環狀多肽,更具體而言環狀十一胺基酸肽(諸如阿拉泊韋)之根據本發明的一般方法;然而,該一般反應圖亦可用於製備環狀多肽,更具體而言衍生自環孢菌素A、B、D或G之環狀十一胺基酸肽。 The following reaction schemes show the general method according to the invention for the preparation of cyclic polypeptides, more particularly cyclic undecyl acid peptides, such as alisporivir; however, the general reaction scheme can also be used to prepare cyclic polypeptides. More specifically, a cyclic undecyl acid peptide derived from cyclosporin A, B, D or G.
具體而言,可如下製備阿拉泊韋:藉由環孢菌素A之醯基化以形成乙醯基-環孢菌素A(2);開環;結晶以獲得化合物3、化合物3之埃德曼降解反應;結晶以獲得化合物4而將環孢菌素A(化合物(1),其中 R2為乙基)轉化成以上所示之式4之化合物,及接著使化合物4環化以形成阿拉泊韋(如下所示)。 Specifically, alisporivir can be prepared by thiolation of cyclosporin A to form acetyl-cyclosporin A (2); ring opening; crystallization to obtain compound 3, compound 3 Deman degradation reaction; crystallization to obtain compound 4 and cyclosporin A (compound (1) wherein R 2 is ethyl) is converted to the compound of formula 4 shown above, and then compound 4 is cyclized to form Alappovir (shown below).
本發明具體係關於各區段中所述之方法。本發明同樣獨立地關於在相應區段內之製程順序中所述的每一單一步驟。因此,文中所述之由某一順序之步驟組成的任何方法的各個及每一單一步驟自身為本發明之一較佳實施例。因此,本發明亦係關於該方法之彼等實施例,據此,可在方法之任何步驟中以中間產物獲得之化合物係用作起始物質。 The invention is particularly directed to the methods described in the various sections. The invention is also independent of each single step described in the sequence of processes within the respective sections. Accordingly, each and every single step of any method described in the sequence of steps is a preferred embodiment of the invention. Accordingly, the present invention is also directed to such embodiments of the process whereby the compound obtained as an intermediate product in any step of the process is used as the starting material.
本發明亦係關於特定開發用於製備根據本發明之化合物的中間產物、其用途及其製備方法。 The invention is also directed to an intermediate product specifically developed for the preparation of a compound according to the invention, its use and a process for its preparation.
應注意,除非另有說明,否則在本申請案中,在一個區段中所做的解釋亦可應用於其他區段。 It should be noted that, in the present application, the explanations made in one section may also be applied to other sections unless otherwise stated.
環孢菌素A、環孢菌素B、環孢菌素D或環孢菌素G可藉由例如發酵法製備。 Cyclosporin A, cyclosporin B, cyclosporin D or cyclosporin G can be prepared, for example, by a fermentation process.
在一個實施例中,本發明係關於一種製備式3之化合物的方法,其包括以下步驟:使環孢菌素A、環孢菌素B、環孢菌素D或環孢菌素G醯基化以形成乙醯基-環孢菌素A、B、D或G;開環;及結晶。 In one embodiment, the invention relates to a process for the preparation of a compound of formula 3, which comprises the steps of: cyclosporin A, cyclosporin B, cyclosporin D or cyclosporin G thiol To form acetamido-cyclosporin A, B, D or G; ring opening; and crystallization.
在一個實施例中,本發明係關於一種製備式4之化合物或其鹽的 方法,其包括使式3之化合物進行埃德曼降解反應(技術中已熟知的一種反應)及使其結晶以獲得式4之化合物。 In one embodiment, the invention relates to a compound of formula 4 or a salt thereof A process comprising subjecting a compound of formula 3 to an Edman degradation reaction (a reaction well known in the art) and crystallizing it to obtain a compound of formula 4.
本發明之另一實施例係關於一種製備式3或式4之化合物的方法,其中環孢菌素A起始物質之純度為>80重量%。 Another embodiment of the invention is directed to a process for the preparation of a compound of formula 3 or formula 4 wherein the cyclosporin A starting material has a purity of > 80% by weight.
本發明之另一實施例係關於一種製備式3或式4之化合物的方法,其中環孢菌素A起始物質之純度為>85重量%。 Another embodiment of the invention is directed to a process for the preparation of a compound of formula 3 or formula 4 wherein the cyclosporin A starting material has a purity of >85% by weight.
本發明之另一實施例係關於一種製備式3或式4之化合物的方法,其中環孢菌素A起始物質之純度為60至80%(以重量%分析)。 Another embodiment of the present invention is directed to a process for the preparation of a compound of Formula 3 or Formula 4 wherein the cyclosporin A starting material has a purity of from 60 to 80% (analyzed by weight).
在以上所示之方法中,涉及新穎及本發明化合物。因此,本發明之其他標的為以下所示之化合物。 Among the methods shown above, novel and inventive compounds are contemplated. Accordingly, other subject matter of the invention is the compounds shown below.
式3之化合物或其鹽,
式4之化合物或其鹽,
式3之化合物或其鹽,
式4之化合物或其鹽,
以下實例代表反應步驟、中間產物及/或本發明之方法的較佳實施例及用於說明本發明而不限制其範圍。 The following examples represent preferred embodiments of the reaction steps, intermediates, and/or methods of the invention and are intended to illustrate the invention without limiting its scope.
利用米爾文(Merwein)鹽製備化合物3 HBF4鹽 Preparation of Compound 3 HBF 4 Salt Using Merwein Salt
在20-25℃下,使乙醯基-環孢菌素A(100g按現狀)與四氟硼酸三甲基氧鎓(32g)在二氯甲烷(180mL)中反應。20h之後,添加乙腈(200mL)及水(650mL)以進行水解。3h之後,在20-25℃下,分離相及藉由利用2-甲基-四氫呋喃(溶劑交換二氯甲烷/2-甲基-四氫呋喃)之共沸蒸餾乾燥反應混合物。然後,使所需產物自2-甲基-四氫呋喃(900 mL)及2-甲氧基-2-甲基丙烷(400mL)結晶以提供呈白色晶型粉末之化合物3 HBF4(63.9g,乾燥之後,純度>92%)。0.69,(3H,d,J=6.6Hz);0.71,(3H,d,J=6.5Hz);0.81,(6H,m);[0.82..0.89],(24H,m);0.90,(3H,d,J=6.6Hz);0.93,(3H,d,J=6.6Hz);1.16,(6H,m);[1.23..1.50],(4H,m);1.52,(1H,m);[1.32..1.73],(8H,m);1.59,(3H,d,J=6.0Hz);1.65,(2H,m);1.65,2.13,(2H,m);1.93,1.94,(3H,s);2.03,(1H,m);2.19,(1H,m);2.45,(3H,s);2.72,(3H,s);2.84,(3H,s);2.86,(3H,s);2.99,(3H,s);3.02,(3H,s);3.06,(3H,s);3.62,3.68,(3H,s);3.78,(1H,m);3.87,4.53,(1H,d,J=17.2Hz,18.6Hz);4.10,4.26,(1H,d,J=18.6Hz,16.8Hz);4.23,(1H,m);4.60,(1H,m);4.62,(1H,m);4.66,(1H,m);5.02,(1H,m);5.13,(1H,dd,J=11.3Hz,4.7Hz);5.26,(1H,m);5.29,(1H,m);5.32,(1H,m);5.36,(1H,m);5.39,(2H,m);7.72,(1H,d,J=7.3Hz);8.14,(1H,d,J=7.3Hz);8.21,8.35,(1H,d,J=7.3Hz,8.1Hz);8.85,(2H,s,br);8.96,(1H,d,J=8.4Hz)。 Ethyl-cyclosporin A (100 g as present) was reacted with trimethyloxonium tetrafluoroborate (32 g) in dichloromethane (180 mL) at 20-25 °C. After 20 h, acetonitrile (200 mL) and water (650 mL) were added for hydrolysis. After 3 h, the phases were separated and the reaction mixture was dried by azeotropic distillation using 2-methyl-tetrahydrofuran (solvent exchange dichloromethane/2-methyl-tetrahydrofuran) at 20-25 °C. Then, the desired product was crystallized from 2-methyl-tetrahydrofuran (900 mL) and 2-methoxy-2-methylpropane (400 mL) to afford compound 3 HBF 4 (63.9 g, dry After that, the purity was >92%). 0.69, (3H, d, J = 6.6 Hz); 0.71, (3H, d, J = 6.5 Hz); 0.81, (6H, m); [0.82..0.89], (24H, m); 0.90, ( 3H,d,J=6.6Hz);0.93,(3H,d,J=6.6Hz); 1.16,(6H,m);[1.23..1.50],(4H,m);1.52,(1H,m ); [1.32..1.73], (8H, m); 1.59, (3H, d, J = 6.0 Hz); 1.65, (2H, m); 1.65, 2.13, (2H, m); 1.93, 1.94, (3H, s); 2.03, (1H, m); 2.19, (1H, m); 2.45, (3H, s); 2.72, (3H, s); 2.84, (3H, s); 2.86, (3H , s); 2.99, (3H, s); 3.02, (3H, s); 3.06, (3H, s); 3.62, 3.68, (3H, s); 3.78, (1H, m); 3.87, 4.53, (1H, d, J = 17.2 Hz, 18.6 Hz); 4.10, 4.26, (1H, d, J = 18.6 Hz, 16.8 Hz); 4.23, (1H, m); 4.60, (1H, m); 4.62, (1H, m); 4.66, (1H, m); 5.02, (1H, m); 5.13, (1H, dd, J = 11.3 Hz, 4.7 Hz); 5.26, (1H, m); 5.29, (1H , m); 5.32, (1H, m); 5.36, (1H, m); 5.39, (2H, m); 7.72, (1H, d, J = 7.3 Hz); 8.14, (1H, d, J = 7.3 Hz); 8.21, 8.35, (1H, d, J = 7.3 Hz, 8.1 Hz); 8.85, (2H, s, br); 8.96, (1H, d, J = 8.4 Hz).
利用原甲酸三甲酯及三氟化硼合乙醚製備化合物3 HBF4鹽 Preparation of Compound 3 HBF 4 Salt by Trimethyl orthoformate and Boron Trifluoride
在-15℃下,將含於二氯甲烷(20mL)中之乙醯基-環孢菌素A(10g)之溶液添加至四氟硼酸二甲氧基碳之漿液中,該漿液係在-20℃下,藉由將三氟化硼(2ml)緩慢添加至含於二氯甲烷(20mL)中之原甲酸三甲酯(2ml)之溶液中而產生。添加之後,漿液可升溫至室溫及保持攪拌20h。之後,添加乙腈(10ml)及水(10ml)。在0℃下攪拌2h之後,相分離。接著,利用水洗滌有機相之後,將溶劑換成2-甲基-四氫呋喃及利用2-甲氧基-2-甲基丙烷飽和,獲得呈白色固體之化合物3,其在真空下乾燥(5.1g,>90%純度)(參見圖1)。 A solution of ethyl-cyclosporin A (10 g) in dichloromethane (20 mL) was added to a slurry of difluoroboric acid dimethoxycarbon at -15 ° C. It was produced by slowly adding boron trifluoride (2 ml) to a solution of trimethyl orthoformate (2 ml) in dichloromethane (20 mL) at 20 °C. After the addition, the slurry was allowed to warm to room temperature and kept stirring for 20 h. After that, acetonitrile (10 ml) and water (10 ml) were added. After stirring at 0 ° C for 2 h, the phases were separated. Next, after washing the organic phase with water, the solvent was replaced with 2-methyl-tetrahydrofuran and saturated with 2-methoxy-2-methylpropane to obtain Compound 3 as a white solid, which was dried under vacuum (5.1 g) , >90% purity) (see Figure 1).
化合物HBF4鹽之製法: Method for preparing compound HBF 4 salt:
將之前製備之化合物3之鹽(34.62g)與碳酸鈉(4.8g)、甲苯(50mL)及水(50mL)一起加入反應器。在20-25℃下攪拌所得混合物30分 鐘,及相分離。在20-25℃下,歷時1h滴加異硫氰酸苯酯(3.81g)及攪拌所得反應混合物直到完成。接著,添加甲醇(20mL)及48%氟硼酸水溶液(2.5g)及另外攪拌混合物1h。然後,添加水(25mL),及相分離。再次利用甲苯(50mL)萃取含水層及接著利用2-甲基-四氫呋喃(100mL)萃取。共沸乾燥有機萃取物及使所需產物自2-甲基-四氫呋喃(100mL)及2-甲氧基-2-甲基丙烷(50mL)結晶以提供呈白色晶型粉末之化合物4 HBF4。(約30g,乾燥之後,純度>93%)。(參見圖2)。 The previously prepared salt of compound 3 (34.62 g) was charged to the reactor along with sodium carbonate (4.8 g), toluene (50 mL) and water (50 mL). The resulting mixture was stirred at 20-25 ° C for 30 minutes and phase separated. Phenyl isothiocyanate (3.81 g) was added dropwise at 20-25 ° C over 1 h and the resulting reaction mixture was stirred until completion. Next, methanol (20 mL) and a 48% aqueous solution of fluoroboric acid (2.5 g) were added and the mixture was further stirred for 1 h. Then, water (25 mL) was added, and the phases were separated. The aqueous layer was extracted again with toluene (50 mL) and then extracted with 2-methyl-tetrahydrofuran (100 mL). The organic extract was azeotropically dried and the desired product was crystallised from 2-methyl-tetrahydrofuran (100 mL) and 2-methoxy-2-methylpropane (50 mL) to afford Compound 4 HBF 4 as a white crystalline powder. (about 30 g, after drying, purity >93%). (See Figure 2).
0.69,(3H,d,J=6.2Hz);0.73,(3H,d,J=7.0Hz);0.81,(3H,t,J=7.3Hz,7.3Hz);0.82,(3H,m);0.85,(9H,m);0.88,(6H,m);0.91,(3H,d,J=7.0Hz);0.93,(3H,d,J=6.6Hz);0.99,(3H,d,J=7.0Hz);1.17,(6H,d,J=6.6Hz);[1.30..1.55],(9H,m);1.60,(3H,d,J=5.5Hz);[1.56..1.72],(4H,m);1.93,1.95(3H,s);2.09,(1H,m);2.14,(1H,m);2.20,(1H,m);2.74,(3H,s);2.82,3.06,(3H,s);2.84,(3H,s);2.87,(3H,s);2.94,(3H,s);3.02,(3H,s);3.63,3.68,(3H,s);3.88,4.52,(1H,d,J=17.2Hz,18.6Hz);4.10,4.24,(1H,d,J=18.7Hz,m);4.24,(2H,m);4.39,4.62,(1H,m);4.66,(1H,m);5.02,(1H,m);5.08,(1H,m);5.26,(2H,m);5.32,(1H,m);5.37,(1H,m);5.39,(2H,m);7.84,8.51(1H,d,J=7.3Hz,8.1Hz);7.98,(3H,s,br);8.07,8.18(1H,d,J=7.7Hz,7.3Hz);8.13,8.27,(1H,d,J=7.3Hz,8.1Hz)。 0.69, (3H, d, J = 6.2 Hz); 0.73, (3H, d, J = 7.0 Hz); 0.81, (3H, t, J = 7.3 Hz, 7.3 Hz); 0.82, (3H, m); 0.85, (9H, m); 0.88, (6H, m); 0.91, (3H, d, J = 7.0 Hz); 0.93, (3H, d, J = 6.6 Hz); 0.99, (3H, d, J =7.0 Hz); 1.17, (6H, d, J = 6.6 Hz); [1.30..1.55], (9H, m); 1.60, (3H, d, J = 5.5 Hz); [1.56..1.72] , (4H, m); 1.93, 1.95 (3H, s); 2.09, (1H, m); 2.14, (1H, m); 2.20, (1H, m); 2.74, (3H, s); 3.06, (3H, s); 2.84, (3H, s); 2.87, (3H, s); 2.94, (3H, s); 3.02, (3H, s); 3.63, 3.68, (3H, s); 3.88, 4.52, (1H, d, J = 17.2 Hz, 18.6 Hz); 4.10, 4.24, (1H, d, J = 18.7 Hz, m); 4.24, (2H, m); 4.39, 4.62, (1H, m); 4.66, (1H, m); 5.02, (1H, m); 5.08, (1H, m); 5.26, (2H, m); 5.32, (1H, m); 5.37, (1H, m) ; 5.39, (2H, m); 7.84, 8.51 (1H, d, J = 7.3 Hz, 8.1 Hz); 7.98, (3H, s, br); 8.07, 8.18 (1H, d, J = 7.7 Hz, 7.3 Hz); 8.13, 8.27, (1H, d, J = 7.3 Hz, 8.1 Hz).
阿拉泊韋之製法 Alabome's method of production
在15℃下,將前述之中間產物4(約109g)按份數添加至甲苯及碳酸鈉/水之混合物中並在15℃下攪拌3小時。分離水相。在0℃下,添加二肽(約28g)及N-羥基苯并三唑單水化物(8.1g)。將水(2.5mL)添加至混合物並在-10℃下配量加入N-甲基嗎啉(17.9g),接著在-10℃下配量加入含於甲苯中之二環己基碳二醯亞胺(21.9g)之溶液並在該溫度下攪拌3小時。歷時10小時將反應混合物加熱至0℃。在完成時,過濾反應混合物及利用5%碳酸鈉溶液、5%鹽溶液、2M鹽酸及10%鹽溶液 萃取濾液。再次過濾有機相及在50℃真空下濃縮。 The aforementioned intermediate product 4 (about 109 g) was added in portions to a mixture of toluene and sodium carbonate/water at 15 ° C and stirred at 15 ° C for 3 hours. Separate the aqueous phase. A dipeptide (about 28 g) and N-hydroxybenzotriazole monohydrate (8.1 g) were added at 0 °C. Water (2.5 mL) was added to the mixture and N-methylmorpholine (17.9 g) was added at -10 °C, followed by dosing at -10 °C to dicyclohexylcarbodiimide contained in toluene. A solution of the amine (21.9 g) was stirred at this temperature for 3 hours. The reaction mixture was heated to 0 °C over 10 hours. Upon completion, filter the reaction mixture and use 5% sodium carbonate solution, 5% salt solution, 2M hydrochloric acid and 10% salt solution The filtrate was extracted. The organic phase was again filtered and concentrated under vacuum at 50 °C.
在20至40℃下,將硼氫化鈉(0.59g)溶於二乙二醇二甲醚(14.3g)。將混濁溶液冷卻至12-16℃。在該溫度下添加甘胺酸(0.59g)。在12-16℃下,將含於約6g甲苯中之先前製備之產物(6.2g)之溶液配量加入至白色懸浮液。接著,在12-16℃下,藉由添加含於甲苯中之甲醇加速還原反應。此添加係經控制並分3份實施。另外攪拌反應3小時,及在10-20℃之內部溫度下添加至中止溶液(乙酸水溶液)。添加的速度與氫氣逸出一致性(無積聚)。分離相,利用水萃取上層有機產物相及隨後濃縮。 Sodium borohydride (0.59 g) was dissolved in diethylene glycol dimethyl ether (14.3 g) at 20 to 40 °C. The turbid solution was cooled to 12-16 °C. Glycine (0.59 g) was added at this temperature. A solution of the previously prepared product (6.2 g) contained in about 6 g of toluene was added to the white suspension at 12-16 °C. Next, the reduction reaction was accelerated by adding methanol contained in toluene at 12-16 °C. This addition was controlled and carried out in 3 parts. Further, the reaction was stirred for 3 hours, and added to a stop solution (aqueous acetic acid solution) at an internal temperature of 10 to 20 °C. The rate of addition is consistent with hydrogen evolution (no accumulation). The phases were separated and the upper organic product phase was extracted with water and subsequently concentrated.
在50℃下,將之前製備之產物(5g)溶於甲苯(約5g)中及歷時40至60分鐘配量加入至含於甲醇(50mL)中之硫酸(0.8g)溶液中。在約2小時之後,將溶液冷卻至15-20℃及配量加入含於甲醇中之25%苄基三甲基氫氧化銨(約12g)(放熱反應)。2小時之後,配量加入水及在22℃下攪拌混合物約20小時。在完成時,將溶液冷卻至10-15℃,利用水稀釋及利用稀硫酸中和。在分離頂層甲苯相之後,藉由蒸餾作用移除底層產物相之甲醇。利用乙酸乙酯萃取油狀分離產物及利用水及鹽溶液按序洗滌,利用稀硫酸將pH調節至7.0-7.5。接著,共沸乾燥有機相及然後在0-5℃冷庚烷上沉澱。過濾產物懸浮液、利用庚烷洗滌及在60℃真空下乾燥。 The previously prepared product (5 g) was dissolved in toluene (about 5 g) at 50 ° C and added to a solution of sulfuric acid (0.8 g) in methanol (50 mL) over a period of 40 to 60 minutes. After about 2 hours, the solution was cooled to 15-20 ° C and 25% benzyltrimethylammonium hydroxide (about 12 g) in methanol was added in an amount (exothermic reaction). After 2 hours, water was added in an amount and the mixture was stirred at 22 ° C for about 20 hours. Upon completion, the solution was cooled to 10-15 ° C, diluted with water and neutralized with dilute sulfuric acid. After separating the top toluene phase, the methanol of the bottom product phase is removed by distillation. The oily product was extracted with ethyl acetate and washed sequentially with water and a salt solution, and the pH was adjusted to 7.0-7.5 with dilute sulfuric acid. Next, the organic phase was azeotropically dried and then precipitated on cold heptane at 0-5 °C. The product suspension was filtered, washed with heptane and dried under vacuum at 60 °C.
在40℃下,歷時約10h,將溶於二氯甲烷中之「十一胺基酸肽胺基酸」前驅物(5至13%之最終總質量)及溶於二氯甲烷之DCC並聯地連續添加至含於二氯甲烷中之Cl-HOBT及NMM的混合物中。在添加末,另外攪拌混合物2h,過濾以除去DCU鹽及濃縮以產生呈粗產物之阿拉泊韋。 The "undecyl-acid peptide amino acid" precursor (5 to 13% of the final total mass) dissolved in methylene chloride and DCC dissolved in methylene chloride were connected in parallel at 40 ° C for about 10 h. It was continuously added to a mixture of Cl-HOBT and NMM contained in dichloromethane. At the end of the addition, the mixture was additionally stirred for 2 h, filtered to remove the DCU salt and concentrated to give the crude product of alisporide.
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- 2013-05-08 SG SG11201406303XA patent/SG11201406303XA/en unknown
- 2013-05-08 WO PCT/EP2013/059672 patent/WO2013167703A1/en active Application Filing
- 2013-05-08 JP JP2015510823A patent/JP2015517481A/en not_active Withdrawn
- 2013-05-08 CN CN201380023760.8A patent/CN104284902A/en active Pending
- 2013-05-08 TW TW102116414A patent/TW201350508A/en unknown
-
2014
- 2014-09-30 TN TNP2014000411A patent/TN2014000411A1/en unknown
- 2014-10-30 IL IL235428A patent/IL235428A0/en unknown
- 2014-11-07 CL CL2014003014A patent/CL2014003014A1/en unknown
- 2014-11-10 CO CO14248207A patent/CO7141428A2/en unknown
- 2014-11-10 PH PH12014502499A patent/PH12014502499A1/en unknown
- 2014-12-08 EC ECIEPI201430537A patent/ECSP14030537A/en unknown
-
2015
- 2015-03-20 HK HK15102858.0A patent/HK1202555A1/en unknown
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2016
- 2016-06-30 US US15/198,152 patent/US9840534B2/en not_active Expired - Fee Related
- 2016-08-31 AU AU2016222370A patent/AU2016222370B2/en not_active Ceased
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2017
- 2017-08-29 JP JP2017164867A patent/JP2018035154A/en not_active Withdrawn
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2019
- 2019-09-30 JP JP2019179311A patent/JP2020033349A/en active Pending
Also Published As
Publication number | Publication date |
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MX2014013613A (en) | 2015-02-12 |
AR090964A1 (en) | 2014-12-17 |
WO2013167703A9 (en) | 2014-11-20 |
CN108715606A (en) | 2018-10-30 |
IN2014DN08483A (en) | 2015-05-08 |
AU2013257989A1 (en) | 2014-10-23 |
EP2847211A1 (en) | 2015-03-18 |
HK1202555A1 (en) | 2015-10-02 |
US20150087808A1 (en) | 2015-03-26 |
WO2013167703A1 (en) | 2013-11-14 |
ECSP14030537A (en) | 2015-09-30 |
US20160304554A1 (en) | 2016-10-20 |
JP2020033349A (en) | 2020-03-05 |
EA201492036A1 (en) | 2015-02-27 |
AU2016222370B2 (en) | 2017-10-05 |
SG11201406303XA (en) | 2014-11-27 |
JP2015517481A (en) | 2015-06-22 |
IL235428A0 (en) | 2014-12-31 |
PE20142433A1 (en) | 2015-02-02 |
BR112014027648A2 (en) | 2017-06-27 |
TN2014000411A1 (en) | 2015-12-21 |
MA20150231A1 (en) | 2015-07-31 |
JP2018035154A (en) | 2018-03-08 |
KR20150006435A (en) | 2015-01-16 |
CO7141428A2 (en) | 2014-12-12 |
US9840534B2 (en) | 2017-12-12 |
CN104284902A (en) | 2015-01-14 |
PH12014502499A1 (en) | 2014-12-22 |
CL2014003014A1 (en) | 2015-03-06 |
AU2016222370A1 (en) | 2016-09-15 |
EA024903B1 (en) | 2016-10-31 |
CA2868940A1 (en) | 2013-11-14 |
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